EP0943662B1 - Kontinuierliches Verfahren zur Herstellung von Farbstoffzusammensetzungen auf Basis von Polymeren - Google Patents

Kontinuierliches Verfahren zur Herstellung von Farbstoffzusammensetzungen auf Basis von Polymeren Download PDF

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Publication number
EP0943662B1
EP0943662B1 EP19990810207 EP99810207A EP0943662B1 EP 0943662 B1 EP0943662 B1 EP 0943662B1 EP 19990810207 EP19990810207 EP 19990810207 EP 99810207 A EP99810207 A EP 99810207A EP 0943662 B1 EP0943662 B1 EP 0943662B1
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EP
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Prior art keywords
pigment
monomer
mixture
initiator
tert
Prior art date
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EP19990810207
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English (en)
French (fr)
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EP0943662A1 (de
Inventor
Johannes Leugs
Harald Marinus Alexander Heere
Adrianus Hendrikus Van Rooijen
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BASF Schweiz AG
Ciba SC Holding AG
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Ciba Spezialitaetenchemie Holding AG
Ciba SC Holding AG
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Priority to EP19990810207 priority Critical patent/EP0943662B1/de
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/44—Polymerisation in the presence of compounding ingredients, e.g. plasticisers, dyestuffs, fillers
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09B—ORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B67/00—Influencing the physical, e.g. the dyeing or printing properties of dyestuffs without chemical reactions, e.g. by treating with solvents grinding or grinding assistants, coating of pigments or dyes; Process features in the making of dyestuff preparations; Dyestuff preparations of a special physical nature, e.g. tablets, films
    • C09B67/006—Preparation of organic pigments
    • C09B67/0063—Preparation of organic pigments of organic pigments with only macromolecular substances

Definitions

  • the present invention relates to an improved process for preparing pigment preparations by mixing a dyestuff with a monomer and simultaneously polymerizing the monomers in an extruder at elevated temperatures.
  • pigment preparations In view of the strong tendency towards improved industrial hygiene, customers are more and more switching from powder pigments towards the use of pigment preparations.
  • Pigment preparations do consist of pigment on the one hand and a carrier material on the other. Consequently, by using pigment preparations, carrier material together with the pigment are introduced into the applications system.
  • carrier material In order to minimise possible effects of the carrier material in the end application, its concentration should be as low as possible, or, in other words, the pigment concentration should be as high as possible, while maintaining optimal dispersion properties.
  • EP-A 456 610 and EP-A 542 669 describe a process for the manufacture of pigment preparations comprising up to 10% by weight of a coloured composition but all in polycondensation resins, such as thermoset crosslinked resins (bulk condensation of a sulphonamide with an aldehyde) and polyamide, polyester, polycarbonate or polyurethane resins respectively, whereby the reactants (monomers) for the formation of said polycondensation resin are introduced continuously together with the coloured composition into an extruder and polymerised therein at elevated temperatures.
  • polycondensation resins such as thermoset crosslinked resins (bulk condensation of a sulphonamide with an aldehyde) and polyamide, polyester, polycarbonate or polyurethane resins respectively, whereby the reactants (monomers) for the formation of said polycondensation resin are introduced continuously together with the coloured composition into an extruder and polymerised therein at elevated temperatures.
  • a major drawback of these processes is the fact that only up to 10% of a colored composition can be incorporated into the polycondensation resins.
  • a further drawback is, that the polydispersity M w /M n is too high, because for a lot of applications a narrow distribution is preferred. For some applications, too, polymers with low molecular weights are desired.
  • the object of this invention was to provide a process yielding pigment preparations which contain more than 10% of pigment and exhibit an improved polydispersity.
  • pigment preparations should be provided wherein the polymers do have a low molecular weight.
  • the monomer component (b) is admixed with either
  • the admixture can be carried out by known methods e.g. by mixing the components in usual vessels and agitators, static mixers etc.
  • the initiator or mixture of initiators (c) is admixed with the monomer component (b) with or without the chain transfer agent (d)
  • Pigments which can be used according to the instant invention are any of the solid colorants normally used in the industry for the colouring of high molecular organic material. These include organic pigments and inorganic pigments as well as carbon black. Typical organic pigments are those of the quinacridone, diketopyrrolopyrrole, anthraquinone, perylene, indigo, quinophthalone, isoindolinone, isoindoline, dioxazine, phthalocyanine or azo series, or a mixture thereof.
  • suitable inorganic pigments are metal oxide pigments, such as iron oxide, titanium oxide and chromium oxide, cadmium pigments, such as cadmium sulfide, bismuth pigments, such as bismuth vanadate, chromate pigments, such as lead chromate, molybdate pigments, such as lead molybdate, and the like, or a mixture thereof. Mixtures of all kinds of pigments can also be used.
  • the amount of pigment to be introduced into the extruder is chosen in the range of from 40 to 90, preferably from 40 to 80, more preferably from 45 to 80, most preferably from 45 to 75% by weight, based on the total amount of introduced pigment and monomer(s).
  • the amount of pigment in the pigment preparation usually - depending inter alia on the degree of polymerization - is within the range of from 40 to 90, preferably from 50 to 75, and in some cases it can be as high as from 60 to 75% by weight, based on the total composition.
  • the monomer or monomer mixture is selected from the group consisting of
  • Suitable C 1 -C 12 alkyl groups are methyl, ethyl, n-propyl, isopropyl, n-butyl, sec.-butyl, i-butyl, tert.-butyl, amyl, hexyl, heptyl, octyl, 2-ethylhexyl, nonyl, decyl or dodecyl, preferably C 1 -C 4 alkyl such as methyl, ethyl, n-propyl, isopropyl, n-butyl, sec.-butyl, i-butyl or tert.-butyl, more preferably methyl, ethyl and n-butyl.
  • prepolymers obtained from the above-mentioned monomers can be used, too.
  • Preferred acrylate monomers are those of formula I, wherein R 1 is hydrogen or methyl and R 2 is C 1 -C 4 alkyl, or a mixture thereof.
  • a preferred embodiment of this invention uses mixtures of methylmethacrylate (“MMA”) and n-butylacrylate (“BA”), methylmethacrylate and styrene (“S”), and methylmethacrylate and n-butylacrylate and acrylic acid (“AA”).
  • Mixtures of MMA/S usually contain from 90 to 60% b.w. MMA and from 10 to 40% S, and mixtures of MMA/BA/AA usually contain from 50 to 80% b.w. MMA, 10 to 40% b.w. BA and from 5 to 30% AA, the total amounts always sum up to 100%.
  • mixtures of methylmethacrylate and butylacrylate preferably from 40 to 80% b.w. of MMA and from 60 to 20% b.w. of BA, more preferably from 50 to 75% b.w. of MMA and from 50 to 25% b.w. of BA, most preferably from 60 to 75% b.w. of MMA and from 40 to 25% b.w. of BA, the total amounts always sum up to 100%.
  • the amount of monomer component (b) is within the range of from 60 to 10, preferably from 50 to 25, and in some cases it can be as low as from 40 to 25% by weight, based on the total composition. Accordingly, the amount of polymer in the pigment preparation usually is within the range of 60 to 10, preferably from 50 to 25, and in some cases it can be as low as from 40 to 25% by weight, based on the total composition, depending inter alia on the degree of polymerization.
  • the initiators to be used for the present invention in general are the initiators commonly used for polymerisations e.g. peroxydes, peresters, hydroperoxydes and some azo compounds and also mixtures thereof.
  • Preferred initiators are selected from the group consisting of tert.-butyl peroxyneodecanoate (TBPND), tert.-butylperoxyethylhexylcarbonate (TBPEHC) tert.-amylperoxyneodecanoate (TAPND), tert.-amylperoxypivalate (TAPPI), tert.-butylperoxypivalate (TBPPI), 2,5-dimethyl-2,5-di(2-ethylhexanoylperoxy)hexane (DHPEH), tert.-amylperoxy-2-ethylhexanoate (TAPEH), tert.-butylperoxy-2-ethylhexanoate (TBPEH), tert.-butylperoxy-3,5,5-trimethylhexanoate (TBPIN) and mixtures thereof.
  • TBPND tert.-butyl peroxyne
  • mixtures of tert.-butylperoxyneodecanoate and tert.-butylperoxy-ethylhexylcarbonate preferably chosen in the range of from 50 to 90% b.w. TBPND and 50 to 10% b.w. TBPEHC, the total sum being 100%, especially preferred is a weight ratio of in the range of from (70 to 80)/(30 to 20) (TBPND/TBPEHC).
  • the amount of initiator or mixture of initiators usually is chosen in the range of from 0.01 to 10%, preferably from 2 to 8% and most preferably 3 to 6% by weight, based on the monomer or monomer mixture.
  • a chain transfer agent, component (d) is used in amounts preferably in the range of from 0.01 to 10, more preferred from 0.1 to 5, most preferred from 1 to 4% by weight, related to the amount of monomer component (b).
  • chain transfer agents or also commonly known as molecular weight regulators, all known compounds such as primary C 1 -C 15 alkyl mercaptans like n-butyl mercaptan, sec.-butyl mercaptan, tert.-butyl mercaptan, n-dodecyl mercaptan, i-dodecyl mercaptan, tert.-dodecyl mercaptan, preferred are n-butyl mercaptan, sec.-butyl mercaptan, tert.-butyl mercaptan, n-dodecyl mercaptan and tert.-dodecyl mercaptan
  • solvents such as organic solvents such as halogenated hydrocarbons like tetrachloro methane, ethers like tetrahydrofurane, ketones like methyl-isobutyl ketone, aromatic hydrocarbons such as benzene, toluene, xylene can be used as chain transfer agents, too.
  • the usual additives and fillers such as crystal growth inhibitors usually in amounts in the range of from 0.01 to 15% by weight, related to the total amount of reactants, rheology improvers usually in amounts ranging from 0.01 to 15% by weight, related to the total amount of reactants, dispersants usually in amounts in he range of from 0.01 to 30% by weight, related to the total amount of reactants, and stabilizers and antioxidants in effective amounts may be added.
  • the reaction temperature usually should be chosen sufficiently high to ensure that the polymerization reaction takes place in a reasonable time. In general, this depends of course from the chosen reactants, but can be figured out easily by a person skilled in the art, because the corresponding data are well-known in the art.
  • the reaction can be carried out at from 70 to 220°C, preferably from 90 to 200°C.
  • the reaction can be carried out at a temperature in the range of from 100 to 170°C.
  • the reaction time depends on the chosen reactants, the desired molecular weight of the polymer to be produced, the chosen reaction temperature, etc. Suitable reaction times can be found easily by a person skilled in the art, if necessary by a few pilot tests. As an example, in case a MMA/BA mixture (7:3) and a diketopyrrolopyrrol as pigment, the reaction time usually is within the range of 0.1 to 2 hours, if the reaction temperature is within the range of from 50 to 150°C.
  • any kind of extruder can be used, e.g. twin-screw extruders or kneading extruders, but co-rotating twin-screw extruders and especially co-rotating, closely intermeshing extruders are preferred.
  • a co-rotating twin-screw extruder is used with a L/D (length/diameter) ratio in the range of from 30 to 60, particularly from 40 to 60.
  • the throughputs in the extruder depend on the different reactants and, of course, on the size of the extruder.
  • the throughput is preferably chosen in the range of from 0.1 to 10, more preferred from 1 to 8 kg/h.
  • a temperature profile is applied to different zones of the used extruder depending on the chosen pigment and monomer.
  • Preferred e.g. is a temperature profile in which
  • the zone of the extruder with the desired highest temperature can be extended, preferably in combination with the overall length L of the extruder, and, of course, more detailed profiles can be chosen, usually depending on the chosen pigments, monomers, initiators, and chain transfer agents.
  • the reaction mixture is withdrawn continuously from the extruder by known methods, e.g. it is usually released into air and/or water at ambient temperature and atmospheric pressure. If desired, further work-up can be carried out such as granulating or pulverizing by known methods to yield granules, powders or pastes, if the powder is mixed with an organic solvent or water.
  • Another embodiment of the present invention is related to the use of the prepared pigment preparations for the preparation of coloring high molecular weight organic materials (usually having a molecular weight in the range of 10 5 to 10 7 g/mol), e.g. biopolymers, plastic materials, including fibres, glasses, ceramic products, for formulations in decorative cosmetics, for the preparation of inks, printing inks, paint systems, in particular automotive lacquers and photoresists, photo- and electroconductive polymers, fluorescent whitening agents, photocell aggregates, colored photoresists, color filters and dispersion colors and, furthermore, the prepared pigment preparations can be used in the biomedical field of application, e.g. for the preparation of diagnostic agents as well as in the fields of impact-printing and non-impact-printing and photo/repro in general.
  • the prepared pigment preparations can be used in the biomedical field of application, e.g. for the preparation of diagnostic agents as well as in the fields of impact-printing and non-impact-printing and photo/re
  • suitable organic materials of high molecular weight which can be colored with the prepared pigment preparations of this invention are vinyl polymers, for example polystyrene, poly- ⁇ -methylstyrene, poly-p-methylstyrene, poly-p-hydroxystyrene, poly-p-hydroxyphenylstyrene, polymethyl methacrylate and polyacrylamide as well as the corresponding methacrylic compounds, polymethylmaleate, polyacrylonitrile, polymethacrylonitrile, polyvinyl chloride, polyvinyl fluoride, polyvinylidene chloride, polyvinylidene fluoride, polyvinyl acetate, polymethyl vinyl ether and polybutyl vinyl ether; polymers which are derived from maleinimide and/or maleic anhydride, such as copolymers of maleic anhydride with styrene; polyvinyl pyrrolidone; ABS; ASA; polyamides; polyimides; polyamidimides
  • cellulose, cellulose ethers and esters such as ethylcellulose, nitrocellulose, cellulose acetate and cellulose butyrate, starch, chitin, chitosan, gelatin, zein; natural resins; synthetic resins such as alkyd resins, acrylic resins, phenolic resins, epoxide resins, aminoformaldehyde resins such as urea/formaldehyde resins and melamine/formaldehyde resin; vulcanized rubber; casein; silicone and silicone resins; rubber, chlorinated rubber; and also polymers which are used, for example, as binders in paint systems, such as novolaks which are derived from C 1 -C 6 -aldehydes such as formaldehyde and acetaldehyde and a binuclear or mononuclear, preferably mononuclear, phenol which, if desired, is substituted by one or two C 1 -C 9 alkyl groups,
  • Particularly preferred high molecular weight organic materials are, for example, cellulose ethers and esters, e.g. ethylcellulose, nitrocellulose, cellulose acetate and cellulose butyrate, natural resins or synthetic resins (polymerization or condensation resins) such as aminoplasts, in particular urea/formaldehyde and melamine/formaldehyde resins, alkyd resins, phenolic plastics, polycarbonates, polyolefins, polystyrene, polyvinyl chloride, polyamides, polyurethanes, polyester, ABS, ASA, polyphenylene oxides, vulcanized rubber, casein, silicone and silicone resins as well as their possible mixtures with one another.
  • cellulose ethers and esters e.g. ethylcellulose, nitrocellulose, cellulose acetate and cellulose butyrate
  • natural resins or synthetic resins polymerization or condensation resins
  • aminoplasts in particular urea/formalde
  • organic materials in dissolved form as film formers, for example boiled linseed oil, nitrocellulose, alkyd resins, phenolic resins, melamine/formaldehyde and urea/formaldehyde resins as well as acrylic resins.
  • film formers for example boiled linseed oil, nitrocellulose, alkyd resins, phenolic resins, melamine/formaldehyde and urea/formaldehyde resins as well as acrylic resins.
  • Said high molecular weight organic compounds may be obtained singly or in admixture, for example in the form of granules, plastic materials, melts or in the form of solutions, in particular for the preparation of spinning solutions, paint systems, coating materials, inks or printing inks.
  • the inventive prepared pigment preparations are used for the mass coloration of polyvinyl chloride, polyamides and, such as polyethylene and polypropylene as well as for the preparation of paint systems, including powder coatings, inks, printing inks, color filters and coating colors.
  • Illustrative examples of preferred binders for paint systems are alkyd/melamine resin paints, acryl/melamine resin paints, cellulose acetate/cellulose butyrate paints and two-pack system lacquers based on acrylic resins which are crosslinkable with polyisocyanate.
  • the prepared pigment preparations can be added in any desired amount to the material to be colored, depending on the end use requirements.
  • the pigments preparations prepared according to this invention can be used in an amount in the range from 0.01 to 40, preferably from 0.1 to 20% by weight, based on the total weight of the colored high molecular weight organic material.
  • composition comprising of
  • the pigmenting of the high molecular weight organic materials with the prepared pigment preparations usually is effected by incorporating said prepared pigment preparations, if desired in the form of masterbatches, in the high molecular weight organic materials using customary apparatus suitable to this end, such as extruders, roll mills, mixing or milling apparatus.
  • the material thus treated is then normally brought into the desired final form by methods which are known per se, such as calandering, moulding, extrusion moulding, coating, casting, extruding, by injection moulding.
  • plasticizers can be added to the high molecular weight substances prior to moulding.
  • Plasticizers may be, for example, esters of phosphoric acid, phthalic acid and sebacic acid. Said plasticizers may be added before, during or after pigmenting the high molecular weight substances with the prepared pigment preparations.
  • the prepared pigment preparations may advantageously be used in admixture with fillers, transparent and opaque white, colored and/or black pigments as well as customary luster pigments in the desired amount.
  • the corresponding high molecular weight organic substances such as binders, synthetic resin dispersions etc. and the prepared pigment preparations are usually dispersed or dissolved together, if desired together with customary additives such as dispersants, fillers, paint auxiliaries, siccatives, plasticizers and/or additional pigments or pigment precursors, in a common solvent or mixture of solvents.
  • customary additives such as dispersants, fillers, paint auxiliaries, siccatives, plasticizers and/or additional pigments or pigment precursors, in a common solvent or mixture of solvents. This can be achieved by dispersing or dissolving the individual components by themselves, or also several components together, and only then bringing all components together, or by adding everything together at once.
  • a further embodiment of the present invention relates to the use of the prepared pigment preparations for the preparation of dispersions and the corresponding dispersions, and paint systems, coating materials, color filters, inks and printing inks comprising the prepared pigment preparations.
  • the prepared pigment preparations exhibit better dispersibility, transparency and color strength compared to corresponding known compositions. Further, the process to obtain the prepared pigment preparations is an easy, industrial applicable one-step process.
  • the preparation consists of tailor-made carrier material in order to guarantee compatibility with paint, plastics and printing ink application systems of individual customers, instead of commercially available carrier materials of which wide compatibility is questionable. Transparent applications can be obtained by the use of the prepared pigment preparations which show the outstanding fastness of pigments. In addition, no solvents are necessary in the one-step process.
  • Monomers (after preparation cooled to -20°C), initiators (cooled to -20°C), and chain transfer agents (ambient temperature) are mixed by manually shaking and stirring and the obtained homogeneous mixture is stored in an atmosphere of nitrogen in a dosing vessel at a temperature in the range of -15 to -5°C.
  • the extruder is divided into 15 zones, including a transition flange and the die-head, all having the same length, and each zone is heated individually.
  • the screw speed is 300 rpm.
  • the melt is degassed in zone 12 at a pressure of 5 mbar (absolute), and extruded and filtered in zone 15.
  • the extrudate is collected in a container, broken and ground.
  • the Table below summarizes the results.
  • Example 4 Example 1 is repeated, but a phthalocyanine (HELIOGEN®Grün K8730 from BASF; C.I.Pigment Green 7) is used instead of the IRGAZIN® pigment, further the temperature profile is as follows:
  • Example 5 Example 2 is repeated, but HELIOGEN®Grün K8730 is used instead of the IRGAZIN® pigment, the temperature profile is the same as in ex. 4.
  • Example 6 Example 3 is repeated, but HELIOGEN®Grün K8730 is used instead of the IRGAZIN® pigment, the temperature profile is the same as in ex. 4.
  • the extruder barrel is divided into 13 zones, all having the same length and a transition flange (zone 14) and the die-head (zone 15) and each zone is heated individually.
  • the screw speed is 300 rpm.
  • the melt is degassed in zone 12 at a pressure of about 5 mbar (absolute).
  • the extrudate is collected in a container, broken and ground.
  • the table below summarizes the results.
  • Example 7 is repeated, but Daihan Blue 8700 is used instead of the IRGAZIN® pigment, further the temperature profile is as follows: zone 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 temperature (°C) 40 40 40 75 110 110 130 140 150 150 150 130 130 150 180
  • Example 8 is repeated, but Daihan Blue 8700 is used instead of the IRGAZIN® pigment, further the temperature profile is the same as in example 10
  • Example 12 (monomer premixed with initiator and chain transfer agent)
  • Example 9 is repeated, but Daihan Blue 8700 is used instead of the IRGAZIN® pigment, further the temperature profile is the same as in example 10.
  • MMA methylmethacrylate
  • BA n-butylacrylate
  • AA acrylic acid
  • the extruder barrel is divided into 13 zones, all having the same length and a transition flange (zone 14) and the die-head (zone 15) and each zone is heated individually.
  • the screw speed is 250 rpm.
  • the melt is degassed in zone 12 at a pressure of about 5 mbar (absolute).
  • the extrudate is collected in a container, broken and ground.
  • the table below summarizes the results.
  • Example 15 (monomer premixed with initiator and chain transfer agent)

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Inks, Pencil-Leads, Or Crayons (AREA)
  • Paints Or Removers (AREA)

Claims (9)

  1. Verfahren zur Herstellung von Pigmentzubereitungen durch Vermischen eines Farbstoffs mit einem Monomer und gleichzeitiges Polymerisieren der Monomere in einem Extruder bei erhöhten Temperaturen, gekennzeichnet durch
    (A) kontinuierliches Einführen in einen Extruder
    (a) 40 bis 90 Gewichtsprozent eines Pigments,
    (b) 60 bis 10 Gewichtsprozent eines Monomers oder eines Monomergemisches und
    (c) 0,01 bis 10 Gewichtsprozent, bezogen auf die Menge an Monomer-Komponente (b), eines Starters oder eines Gemisches von Startern und
    (d) 0 bis 10 Gewichtsprozent, bezogen auf die Menge an Monomer-Komponente (b), eines Kettenübertragungsmittels,
       wobei die Mengen des Pigments und des Monomers oder Monomergemisches sich auf 100% summieren und wobei die Monomer-Komponente (b) entweder mit dem Starter oder Gemisch von Startern (c) oder dem Kettenübertragungsmittel (d) oder dem Starter oder Startergemisch (c) und dem Kettenübertragungsmittel (d) angemischt wird, bevor es in den Extruder eingeführt wird,
    (B) gleichzeitiges Vermischen der Komponenten (a) bis (c) sowie, falls vorliegend, (d) und Polymerisieren des Monomers oder Copolymerisieren des Monomergemisches in dem Extruder und
    (C) kontinuierliches Abziehen des erhaltenen Reaktionsgemisches aus dem Extruder und wobei die erhöhte Temperatur im Bereich von 70 bis 220°C ausgewählt ist.
  2. Verfahren nach Anspruch 1, wobei das Monomer oder die Monomere aus der Gruppe, bestehend aus
       einem Acrylat oder Methacrylat der Formel I CH2=CR1-COOR2    worin R1 Wasserstoff oder Methyl darstellt und R2 Wasserstoff, C1-C12-Alkyl, CH2-CH2-N(R3) (R4), CH2-CH=CH2, CH2CF3, CH2-CH2OR3 oder CH2-CHOH-R3 darstellt,
       R3 und R4 unabhängig voneinander Wasserstoff oder C1-C4-Alkyl darstellen, Acrylnitril, Acrylamid, Styrol, Vinylacetat und Vinylalkohol ausgewählt ist/sind.
  3. Verfahren nach Anspruch 2, dadurch gekennzeichnet, dass ein Acrylatmonomer der Formel I, worin R1 Wasserstoff oder Methyl darstellt und R2 C1-C4-Alkyl darstellt, eingesetzt wird.
  4. Verfahren nach Ansprüchen 1 bis 3, dadurch gekennzeichnet, dass der Starter aus der Gruppe, bestehend aus tert-Butylperoxyneodecanoat, tert-Butylperoxyethylhexylcarbonat, tert-Amylperoxyneodecanoat, tert-Amylperoxypivalat, tert-Butylperoxypivalat, 2,5-Dimethyl-2,5-di(2-ethylhexanoylperoxy)-hexan, tert-Amylperoxy-2-ethylhexanoat, tert-Butylperoxy-2-ethylhexanoat und tert-Butylperoxy-3,5,5-trimethylhexanoat, ausgewählt wird.
  5. Verfahren nach Ansprüchen 1 bis 4, dadurch gekennzeichnet, dass als Pigment ein organisches Pigment einer Chinacridon-, Diketopyrrolopyrrol-, Anthrachinon-, Perylen-, Indigo-, Chinophthalon-, Isoindolinon-, Isoindolin-, Dioxazin-, Phthalocyanin- oder Azo-Reihe oder ein Gemisch davon eingesetzt wird.
  6. Verfahren nach Ansprüchen 1 bis 4, dadurch gekennzeichnet, dass als Pigment ein anorganisches Pigment von einem Metalloxidpigment, ein Cadmiumpigment, ein Chromatpigment, ein Molybdatpigment oder ein Gemisch davon eingesetzt wird.
  7. Pigmentzubereitung, erhältlich gemäß dem Verfahren nach Ansprüchen 1 bis 6.
  8. Organisches Material mit hohem Molekulargewicht, pigmentiert mit einer Pigmentzubereitung, hergestellt gemäß dem Verfahren von Ansprüchen 1 bis 6.
  9. Verwendung einer Pigmentzubereitung, erhalten nach Ansprüchen 1 bis 6, zur Herstellung eines pigmentierten organischen Materials mit hohem Molekulargewicht.
EP19990810207 1998-03-17 1999-03-09 Kontinuierliches Verfahren zur Herstellung von Farbstoffzusammensetzungen auf Basis von Polymeren Expired - Lifetime EP0943662B1 (de)

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JP2000053713A (ja) 1998-03-17 2000-02-22 Ciba Specialty Chem Holding Inc ポリマ―ベ―スの顔料配合物を製造するための連続方法
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